US2019352250A1PendingUtilityA1
Process for the preparation of oxalic acid esters from cesium oxalate
Assignee: SABIC GLOBAL TECHNOLOGIES BVPriority: Jan 30, 2017Filed: Jan 26, 2018Published: Nov 21, 2019
Est. expiryJan 30, 2037(~10.5 yrs left)· nominal 20-yr term from priority
C07C 51/41C07C 67/08
36
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Claims
Abstract
Processes for producing a disubstituted oxalate are disclosed. The process includes contacting a cesium salt with one or more alcohols and carbon dioxide (CO2) under reaction conditions sufficient to produce a composition comprising a disubstituted oxalate.
Claims
exact text as granted — not AI-modified1 . A process for producing a disubstituted oxalate, the process comprising contacting a cesium salt with one or more alcohols and carbon dioxide (CO 2 ) under reaction conditions sufficient to produce a composition comprising a disubstituted oxalate having a general structure of:
where R 1 and R 2 are each independently an alkyl group, a substituted alkyl group, an aromatic group, or a substituted aromatic group.
2 . The process of claim 1 , wherein the reaction conditions comprise a temperature of 125° C. to 200° C.
3 . The process of claim 1 , wherein the reactions conditions comprise a pressure of 2 MPa to 5 MPa.
4 . The process of claim 1 , wherein the cesium salt is cesium oxalate.
5 . The process of claim 4 , wherein the cesium oxalate is obtained by contacting 1 ) CO 2 and carbon monoxide (CO), under reaction conditions sufficient to form a composition comprising the cesium oxalate
6 . The process of claim 5 , wherein the reaction conditions for obtaining the cesium oxalate comprise a reaction temperature of 200° C. to 400° C.
7 . The process of claim 5 , wherein the reaction conditions for obtaining the cesium oxalate comprise providing carbon dioxide at a pressure of 2.0 MPa to 3.0 MPa, and providing carbon monoxide at a pressure of 1.0 MPa to 3 MPa.
8 . The process of claim 7 , wherein the carbon dioxide is contacted with the cesium carbonate at a reaction temperature of 200° C. to 400° C. for at least 1 hour to obtain a cesium carbonate/carbon dioxide reaction mixture, and contacting the cesium carbonate/carbon dioxide reaction mixture with the H 2 at the reaction temperature.
9 . The process of claim 8 , wherein formation of sodium formate is inhibited.
10 . The process of claim 5 , wherein the reaction conditions for obtaining the cesium oxalate comprise providing CO at a pressure of 2 MPa to 6 MPa, preferably about 2 MPa, and providing O 2 at a pressure of 0.05 MPa to 5 MPa.
11 . The process of claim 5 , further comprising isolating the cesium oxalate salt from the product stream prior to converting it to the disubstituted oxalate.
12 . The process of claim 5 , wherein the process is a single reactor synthesis such that cesium oxalate is generated in situ and then contacted with the one or more alcohols and additional CO 2 to produce the disubstituted oxalate.
13 . The process of claim 1 , wherein R 1 and R 2 each independently comprise 1 to 20 carbon atoms.
14 . The process of claim 13 , wherein R 1 and R 2 are each methyl groups.
15 . The process of claim 1 , further comprising isolating the disubstituted oxalate from the product stream.
16 . The process of claim 15 , further comprising reacting the disubstituted oxalate under conditions sufficient to form oxalic acid or ethylene glycol.
17 . A composition for producing a disubstituted oxalate, the composition comprising a cesium salt, carbon dioxide, carbon monoxide, and an alcohol.
18 . The composition of claim 17 , wherein the alcohol is methanol and the disubstituted oxalate is dimethyl oxalate.
19 . A disubstituted oxalate produced by the process of claim 1 .
20 . The disubstituted oxalate of claim 19 , wherein the disubstituted oxalate is dimethyl oxalate.Join the waitlist — get patent alerts
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